EP1920085B1 - Continuous coating process - Google Patents
Continuous coating process Download PDFInfo
- Publication number
- EP1920085B1 EP1920085B1 EP05812128A EP05812128A EP1920085B1 EP 1920085 B1 EP1920085 B1 EP 1920085B1 EP 05812128 A EP05812128 A EP 05812128A EP 05812128 A EP05812128 A EP 05812128A EP 1920085 B1 EP1920085 B1 EP 1920085B1
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- EP
- European Patent Office
- Prior art keywords
- process tank
- tank
- conveyor
- article
- material supply
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- 238000000576 coating method Methods 0.000 title claims abstract description 79
- 238000000034 method Methods 0.000 claims abstract description 220
- 239000011248 coating agent Substances 0.000 claims abstract description 73
- 239000000463 material Substances 0.000 claims abstract description 59
- 238000004891 communication Methods 0.000 claims abstract description 13
- 239000012530 fluid Substances 0.000 claims description 30
- 238000004070 electrodeposition Methods 0.000 claims description 13
- 238000012545 processing Methods 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 239000003973 paint Substances 0.000 claims description 3
- 238000012546 transfer Methods 0.000 claims description 3
- 230000003750 conditioning effect Effects 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/16—Apparatus for electrolytic coating of small objects in bulk
- C25D17/28—Apparatus for electrolytic coating of small objects in bulk with means for moving the objects individually through the apparatus during treatment
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/02—Tanks; Installations therefor
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/06—Suspending or supporting devices for articles to be coated
- C25D17/08—Supporting racks, i.e. not for suspending
Definitions
- the present invention relates to systems and methods of coating articles and, more particularly, to schemes for electro-coating articles in a process tank containing paint or another type of electro-coating medium. Although specific reference is made herein to electro-coating processes, it is contemplated that the present invention will also have applicability to a variety of coating processes.
- EP 0 379648 describes a system for coating small articles comprising a process tank.
- WO 00/06810 describes a system for coating comprising a plurality of process tanks, with an entry port and an exit port, a process conveyor comprising a track and support elements.
- a system for coating comprising: a process tank, the process tank comprising an entry port, an exit port opposite the entry port, and a process path extending from the entry port to the exit port; an open-ended process tank conveyor disposed entirely within the process tank and comprising a track, a plurality of hanger elements coupled to the track and configured to support an article thereon, and hardware characterized by differential movement configured to connect the hanger elements to the track, wherein the track and hanger elements of the conveyor are configured to move-characterized by a tank conveyor path vertically spaced above a return path, wherein the hanger elements are arranged below a process fluid level defined by the process tank; and a coating material supply in communication with the process tank, wherein the coating material supply comprises an overflow tank in fluid communication with the process tank.
- an article coating scheme is provided wherein an "open-ended" process tank conveyor is configured to convey articles to be coated through the process tank of the coating system.
- a method of electrocoating comprising: providing an article with a length that is greater than the maximum length dimension of the process tank; loading the article onto an input conveyor; inputting the article into a process tank through an entry port in the process tank; transferring the article through the process tank by an open-ended process tank conveyor, wherein the open-ended process tank conveyor comprises a track, a plurality of hanger elements coupled to the track and supporting the article thereon, and hardware characterized by differential movement connecting the hanger elements to the track; coating the article with a coating material supply in communication with the process tank as the article is transferred through the process tank characterized by a tank conveyor path vertically spaced above a return path, wherein the hanger elements and the article supported thereon are submerged below the level of coating material in the process tank, wherein the coating material supply comprises an overflow tank in fluid communication with the process tank; outputting the coated article out of the process tank through an exit port in the process tank; and receiving the coated article by an output conveyor adjacent to the
- one object of the present invention is to provide improvements to systems and methods for electrocoating an article.
- Other objects of the present invention will be apparent in light of the description of the invention embodied herein.
- the present invention relates to systems and methods for coating articles of variable length. Although the present invention is described with specific reference to electrocoating processes, coating methods contemplated by the present invention can comprise numerous methods including, but not limited to, electrocoating, electroplating, spray coating, powder coating, and any other suitable coating methods known to one of ordinary skill in the art.
- the system 1 of the present invention comprises a process tank 2, which further includes an entry port 8, and an exit port 9 opposite the entry port 8.
- the process tank 2 further comprises a process path 30 extending from the entry port 8 to the exit port 9.
- the system 1 comprises an open-ended process tank conveyor 6 disposed within the process tank 2.
- an "open-ended" configuration describes a conveyor which comprises an open receiving end 46 and an open dispensing end 48 adapted to receive an article 50 entering the process tank 2, and dispense a coated article 50 exiting the process tank 2.
- Open receiving 46 and dispensing ends 48 receive and dispense articles 50 without regard to the nature of the mechanism utilized to present the article 50 to the conveyor or the device utilized to receive the article 50 dispensed from the conveyor.
- the open-ended process tank conveyor 6 defines a tank conveyor path 32 that extends from the receiving end 46 of the process tank conveyor 6 to a dispensing end 48 of the process tank conveyor 6 along at least a portion of the process path 30.
- Figs. 2 and 5 more clearly illustrate the process path 30 and tank conveyor path 32 in accord with the system 1 of the present invention.
- the process path 30 extends from the entry port 8 of the process tank 2 to the exit port 9 of the process tank 2.
- the process tank conveyor 6 is disposed entirely within the process tank 2, and the tank conveyor path 32 extends along the process path 30. It is contemplated that the tank conveyor path 32 extends beyond either or both of the entry 8/exit 9 ports without departing from the scope of the present invention. It is further contemplated that the tank conveyor path 32 need not reach either the entry 8 or exit 9 ports.
- Figs. 1 and 2 also illustrate the coating material supply 4 for the system 1 of the present invention.
- the coating material supply 4 comprises an overflow tank 5 in fluid communication with the process tank 2.
- the coating material supply 4 further comprises at least one material supply pump 14.
- multiple material supply pumps 14 are used as shown in Fig. 2 .
- the material supply pumps 14 deliver coating material to the process tank 2 to be used in the coating process.
- the coating material may comprise a liquid coat or any suitable fluid material known to one of ordinary skill in the art.
- the system 1 utilizes liquid electrocoat.
- the material supply pumps 14 provide coating material to the process tank 2 at a suitable volumetric material supply flow rate.
- the material supply pumps 14 feed the coating material into the process tank 2 at a flow rate of about 3000 gallons per minute (11356 litre/min).
- a separating wall 16 provides a boundary between the overflow tank 5 and the process tank 2.
- the top of the separating wall 16 defines an overflow portion.
- the overflow portion constitutes an area at the top of the separating wall that extends the length of the separating wall, wherein the overflow portion is configured to allow coating material in the process tank 2 to flow over the separating wall 16 into the overflow tank 5.
- the overflow portion may comprise any suitable structure that allows coating material from the process tank 2 to flow from the process tank 2 into the overflow tank 5.
- the overflow portion may be provided by including a series of openings in the separating wall that permits coating material to flow over, under, or through the separating wall 16 and into the overflow tank 5.
- the overflow portion may be located in another area of the process tank, which is effective in allowing coating material to flow from the process tank into the overflow tank.
- the process tank 2 defines a process fluid level 24.
- the process fluid level 24 is dictated by the entry 8 and exit port 9 and the overflow portion of the separating wall 16.
- the entry port 8 and the exit port 9 are configured to permit fluid contained within the process tank 2 to flow out of the process tank 2 into the overflow tank 5 at a volumetric flow rate that is lower than the volumetric material supply rate.
- the higher volumetric material supply rate ensures that the entry port 8 and exit port 9 are positioned below the process fluid level, which aids in coating.
- the overflow portion in the separating wall 16 allows coating material to flow from the process tank 2 to the overflow tank 5 to prevent flooding.
- the collective volumetric flow rate of the overflow portion and the entry 8 and exit 9 ports is at least as large as the volumetric material supply rate defined by the material supply pump 14. This ensures that the process fluid level 24 will not rise above the overflow portions.
- the process tank 2 defines a process fluid level 24 by including these openings 18 which are configured to remove from the process tank 2 any coating material above this fluid level 24.
- the entry port 8 and exit port 9 can comprise numerous embodiments.
- the entry port 8 includes 2 openings to support the feeding of two articles 50 simultaneously into the process tank 2.
- the openings in the ports can receive an article 50 with a height of about 2 and 1/2 to about 4 inches (about 6.3 to about 10.2 cm), a width of about 6 to about 12 inches, (about 15,3 to about 30,6 cm) and an unlimited and/or variable length.
- the stop gates 17 are located above the entry 8 and exit 9 ports, and are open when the system 1 is operating. When the system 1 is not in use, stop gates 17 arc utilized to close the entry 8 and exit 9 ports.
- the process tank conveyor 2 is positioned below the process fluid level 24 of the process tank 2.
- the process path 30 extends from the entry port 8 of the process tank 2 to the exit port 9 of the process tank 2.
- the process tank conveyor 2 defines a tank conveyor path 32 extending from the receiving end 46 of the process tank conveyor 2 to the dispensing end 48 of the process tank conveyor 6, and a return path 33 extending from the dispensing end 48 of the process tank conveyor 6 to the receiving end 46 of the process tank conveyor 6.
- the tank conveyor path 32 and the return path 33 which is both below the tank conveyor path 32, are positioned below the process fluid level 24 of the process tank 2.
- the process tank conveyor 6 is submerged in a level of coating material equal to the process fluid level 24 inside the process tank when the process tank 2 is in operation.
- the article 50 traveling on the submerged process tank conveyor 6 will also be submerged in a level of coating material equal to the process fluid level 24, which results in the coating of the article 50.
- the process tank conveyor 6 is configured to transfer an article 50 through the process tank 2.
- a process tank conveyor 6 is shown.
- the process tank conveyor 6 comprises a plurality of hanger elements 19, a process tank conveyor track 28, and hardware 26 characterized by differential movement, i.e., parts that move relative to one another.
- the hardware 26 connects the hanger elements 19 to the process tank conveyor track 28.
- the hanger elements 19 are adapted to receive and support the article 50 while the article 50 is transferred through the process tank 2.
- the hanger element 19 comprises two slanted legs 20 connected to a base member 21 with a saw tooth edge 22 on the inner side of the base member 21.
- the article 50 When traveling through the process tank 2 on the process tank conveyor 6, the article 50 rests on the saw tooth edge 22. In addition to electrically grounding the article, the saw tooth edge 22 reduces the amount of surface area in contact with the article 50, as opposed to a flat edge. Thus, the saw tooth edge 22 provides a greater surface area exposed to the coating material within the process tank 2.
- the hanger element utilizes slanted legs 20, because these slanted legs 20 provide improved clearance when traveling in the tank conveyor path 32.
- the process tank conveyor 6 may be configured such that the hanger 19 will remain positioned below the process fluid level 24, while the hardware 26 is located above the process fluid level 24 to prevent hardware malfunction due to coating material build-up or corrosion.
- the process tank 2 comprises at least one electrode 10 configured to provide a charge to the coating material inside the process tank 2.
- the process tank 2 may comprise a plurality of electrodes 10.
- the electrodes 10 are operable for anodic or cathodic coating.
- the process tank conveyor 6 holds the article 50, which typically comprises a rail or other elongated article, at an electrical potential. Under anodic coating, a positively charged article 50 is passed through the process tank 2 on the process tank conveyor 6. To bind the coating material to the article 50, the electrode 10 must provide the coating material 22 with a negative charge, so that the positively charged article 50 may bind with the negatively charged coating. Conversely, under cathodic coating, the process tank 2 receives a negatively charged article 50; therefore, the electrode 10 must provide a positive charge to the coating material 22 to ensure binding between the article 50 and the coating material 22.
- Fig. 3 further illustrates the system 1 of the present invention, wherein an input conveyor 42 and an output conveyor 44 are in communication with the process tank 2.
- the input conveyor 42 is located adjacent to the entry port 8, and the output conveyor 44 is located adjacent to the exit port 9.
- the input 42 and output 44 conveyors define input/output conveyor paths that are independent of the process tank conveyor path. In this manner, the input conveyor 42 and output conveyor 44 operate independently of the process tank 2 and the process tank conveyor 6.
- the input conveyor 42 feeds an article 50 into the entry port 8 of the process tank 6 wherein the article 50 will then be received by the process tank conveyor 6 for coating.
- the output conveyor 44 receives the coated article 50 as it is outputted from the process tank through the exit port 9 by the process tank conveyor 6.
- This three conveyor system comprised of the input conveyor 42, process tank conveyor 6, and the output conveyor 44 enables the system 1 to run continuously without regard to the length of the article 50 being fed into the system 1, or the nature of the input 42 and output 44 conveyors being used.
- a system 1 for electrocoating an article 50 of variable length includes a process tank 2 comprising an entry port 8, and exit port 9 opposite the entry port 8, and a process path 30 extending from the entry port 8 to the exit port 9.
- the process tank 2 further comprises an open-ended process tank conveyor 6 at least partially positioned below a process fluid level 24 defined by the process tank 2.
- the open-ended process tank conveyor 6, which is disposed entirely within the process tank 2, defines a tank conveyor path 32 extending from a receiving end 46 of the process tank conveyor 6 to a dispensing end 48 of the process tank conveyor 6 along at least a portion of the process path 30, wherein the process tank conveyor 2 comprises an open-ended configuration at the receiving end 46 of the process tank conveyor 6 and an open-ended configuration at the dispensing end 48 of the process tank conveyor 6.
- the system 1 also comprises a coating material supply 4 in communication with the process tank 2, an input conveyor 42 adapted to feed the article 50 into the process tank 2, and an output conveyor 44 adapted to receive a coated article 50 from the process tank 2.
- the coating system 1 may comprise additional processing stations for the article 50 being coated.
- the system may incorporate heat exchangers, which are useful in the electrocoating process wherein operating temperatures may vary.
- the system may also include cleaning stations and pretreatment stations to prepare the surface of an article 50 for coating. Pretreatment stations include phosphate baths. Rinsing stations may be incorporated into the system to remove paint solids from the coating, which may affect the efficiency and the aesthetic appeal of the coating.
- the system may also comprise curing ovens, which cures and cross links the coating material after the coating has been applied to assure maximum performance properties of the coating.
- the system may further comprise water conditioning stations, or any other suitable processing station known to one of ordinary skill in the art. All of the processing stations may be used singularly or in combination with the coating system of the present invention.
- a method for electrocoating is provided.
- the coating method is applicable to anodic or cathodic coating.
- the electrocoating method comprises the steps of providing and loading an article 50, such as a rail, onto an input conveyor 42, and subsequently inputting the article 50 into a process tank 2 through an entry port 8. Subsequently, the article 50 is transferred through the process tank 2 by a process tank conveyor 6, wherein the article 50 is simultaneously coated as it moves through the process tank 2. After coating, the process tank conveyor 6 outputs the coated article 50 through an exit port 9 in the process tank 2 wherein the coated article 50 is then received by an output conveyor 44.
- the method incorporates any additional processing steps like pretreating, cleaning, heating, preheating, rinsing, curing, and any combinations thereof.
- device is utilized herein to represent a combination of components and individual components, regardless of whether the components are combined with other components.
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- Coating Apparatus (AREA)
Abstract
Description
- The present invention relates to systems and methods of coating articles and, more particularly, to schemes for electro-coating articles in a process tank containing paint or another type of electro-coating medium. Although specific reference is made herein to electro-coating processes, it is contemplated that the present invention will also have applicability to a variety of coating processes.
-
EP 0 379648 describes a system for coating small articles comprising a process tank. -
WO 00/06810 - In accordance with a first aspect of the present invention there is provided a system for coating comprising: a process tank, the process tank comprising an entry port, an exit port opposite the entry port, and a process path extending from the entry port to the exit port; an open-ended process tank conveyor disposed entirely within the process tank and comprising a track, a plurality of hanger elements coupled to the track and configured to support an article thereon, and hardware characterized by differential movement configured to connect the hanger elements to the track, wherein the track and hanger elements of the conveyor are configured to move-characterized by a tank conveyor path vertically spaced above a return path, wherein the hanger elements are arranged below a process fluid level defined by the process tank; and a coating material supply in communication with the process tank, wherein the coating material supply comprises an overflow tank in fluid communication with the process tank.
- Thus, an article coating scheme is provided wherein an "open-ended" process tank conveyor is configured to convey articles to be coated through the process tank of the coating system.
- In accordance with a further aspect of the present invention there is provided a method of electrocoating comprising: providing an article with a length that is greater than the maximum length dimension of the process tank; loading the article onto an input conveyor; inputting the article into a process tank through an entry port in the process tank; transferring the article through the process tank by an open-ended process tank conveyor, wherein the open-ended process tank conveyor comprises a track, a plurality of hanger elements coupled to the track and supporting the article thereon, and hardware characterized by differential movement connecting the hanger elements to the track; coating the article with a coating material supply in communication with the process tank as the article is transferred through the process tank characterized by a tank conveyor path vertically spaced above a return path, wherein the hanger elements and the article supported thereon are submerged below the level of coating material in the process tank, wherein the coating material supply comprises an overflow tank in fluid communication with the process tank; outputting the coated article out of the process tank through an exit port in the process tank; and receiving the coated article by an output conveyor adjacent to the exit port of the process tank.
- Accordingly, one object of the present invention is to provide improvements to systems and methods for electrocoating an article. Other objects of the present invention will be apparent in light of the description of the invention embodied herein.
- The following detailed description of specific embodiments of the present invention can be best understood when read in conjunction with the following drawings, where like structure is indicated with like reference numerals and in which:
-
Fig. 1 is a side elevation view of an overflow tank, process tank, and process tank conveyor of a coating system according to one embodiment of the present invention. -
Fig. 2 is a top plan view of an overflow tank and process tank of a coating system according to one embodiment of the present invention. -
Fig. 3 is a top plan view of a coating system according to one embodiment of the present invention. -
Fig. 4 is an isometric illustration of a process tank conveyor according to one embodiment of the present invention. -
Fig. 5 is a side elevation view of a coating system according to one embodiment of the present invention. - The present invention relates to systems and methods for coating articles of variable length. Although the present invention is described with specific reference to electrocoating processes, coating methods contemplated by the present invention can comprise numerous methods including, but not limited to, electrocoating, electroplating, spray coating, powder coating, and any other suitable coating methods known to one of ordinary skill in the art.
- Referring to
Figs. 1-5 , thesystem 1 of the present invention comprises aprocess tank 2, which further includes anentry port 8, and anexit port 9 opposite theentry port 8. Theprocess tank 2 further comprises aprocess path 30 extending from theentry port 8 to theexit port 9. Moreover, thesystem 1 comprises an open-endedprocess tank conveyor 6 disposed within theprocess tank 2. For the purposes of defining and describing the present invention, an "open-ended" configuration describes a conveyor which comprises anopen receiving end 46 and anopen dispensing end 48 adapted to receive anarticle 50 entering theprocess tank 2, and dispense a coatedarticle 50 exiting theprocess tank 2. Open receiving 46 and dispensingends 48 receive and dispensearticles 50 without regard to the nature of the mechanism utilized to present thearticle 50 to the conveyor or the device utilized to receive thearticle 50 dispensed from the conveyor. The open-endedprocess tank conveyor 6 defines atank conveyor path 32 that extends from the receivingend 46 of theprocess tank conveyor 6 to a dispensingend 48 of theprocess tank conveyor 6 along at least a portion of theprocess path 30. -
Figs. 2 and5 more clearly illustrate theprocess path 30 andtank conveyor path 32 in accord with thesystem 1 of the present invention. As shown inFig. 2 , theprocess path 30 extends from theentry port 8 of theprocess tank 2 to theexit port 9 of theprocess tank 2. Referring toFig. 5 , theprocess tank conveyor 6 is disposed entirely within theprocess tank 2, and thetank conveyor path 32 extends along theprocess path 30. It is contemplated that thetank conveyor path 32 extends beyond either or both of theentry 8/exit 9 ports without departing from the scope of the present invention. It is further contemplated that thetank conveyor path 32 need not reach either theentry 8 or exit 9 ports. -
Figs. 1 and2 also illustrate thecoating material supply 4 for thesystem 1 of the present invention. Thecoating material supply 4 comprises anoverflow tank 5 in fluid communication with theprocess tank 2. Thecoating material supply 4 further comprises at least onematerial supply pump 14. Typically, multiplematerial supply pumps 14 are used as shown inFig. 2 . Thematerial supply pumps 14 deliver coating material to theprocess tank 2 to be used in the coating process. The coating material may comprise a liquid coat or any suitable fluid material known to one of ordinary skill in the art. Typically, thesystem 1 utilizes liquid electrocoat. Thematerial supply pumps 14 provide coating material to theprocess tank 2 at a suitable volumetric material supply flow rate. For example, and not by way of limitation, in one embodiment of the present invention, thematerial supply pumps 14 feed the coating material into theprocess tank 2 at a flow rate of about 3000 gallons per minute (11356 litre/min). - A separating
wall 16 provides a boundary between theoverflow tank 5 and theprocess tank 2. The top of the separatingwall 16 defines an overflow portion. In one embodiment, the overflow portion constitutes an area at the top of the separating wall that extends the length of the separating wall, wherein the overflow portion is configured to allow coating material in theprocess tank 2 to flow over the separatingwall 16 into theoverflow tank 5. Alternatively, the overflow portion may comprise any suitable structure that allows coating material from theprocess tank 2 to flow from theprocess tank 2 into theoverflow tank 5. For example, the overflow portion may be provided by including a series of openings in the separating wall that permits coating material to flow over, under, or through the separatingwall 16 and into theoverflow tank 5. Moreover, the overflow portion may be located in another area of the process tank, which is effective in allowing coating material to flow from the process tank into the overflow tank. - Referring to
Figs. 1 and2 , theprocess tank 2 defines aprocess fluid level 24. Theprocess fluid level 24 is dictated by theentry 8 andexit port 9 and the overflow portion of the separatingwall 16. Theentry port 8 and theexit port 9 are configured to permit fluid contained within theprocess tank 2 to flow out of theprocess tank 2 into theoverflow tank 5 at a volumetric flow rate that is lower than the volumetric material supply rate. The higher volumetric material supply rate ensures that theentry port 8 andexit port 9 are positioned below the process fluid level, which aids in coating. The overflow portion in the separatingwall 16 allows coating material to flow from theprocess tank 2 to theoverflow tank 5 to prevent flooding. The collective volumetric flow rate of the overflow portion and theentry 8 andexit 9 ports is at least as large as the volumetric material supply rate defined by thematerial supply pump 14. This ensures that theprocess fluid level 24 will not rise above the overflow portions. As a result, theprocess tank 2 defines aprocess fluid level 24 by including these openings 18 which are configured to remove from theprocess tank 2 any coating material above thisfluid level 24. - The
entry port 8 andexit port 9 can comprise numerous embodiments. In one embodiment as shown inFig. 1 , theentry port 8 includes 2 openings to support the feeding of twoarticles 50 simultaneously into theprocess tank 2. Typically, the openings in the ports can receive anarticle 50 with a height of about 2 and 1/2 to about 4 inches (about 6.3 to about 10.2 cm), a width of about 6 to about 12 inches, (about 15,3 to about 30,6 cm) and an unlimited and/or variable length. As shown inFig. 5 , thestop gates 17 are located above theentry 8 and exit 9 ports, and are open when thesystem 1 is operating. When thesystem 1 is not in use,stop gates 17 arc utilized to close theentry 8 and exit 9 ports. - Under one embodiment of the present invention, the
process tank conveyor 2 is positioned below theprocess fluid level 24 of theprocess tank 2. As shown inFig. 2 , theprocess path 30 extends from theentry port 8 of theprocess tank 2 to theexit port 9 of theprocess tank 2. Theprocess tank conveyor 2 defines atank conveyor path 32 extending from thereceiving end 46 of theprocess tank conveyor 2 to the dispensingend 48 of theprocess tank conveyor 6, and areturn path 33 extending from the dispensingend 48 of theprocess tank conveyor 6 to thereceiving end 46 of theprocess tank conveyor 6. Typically, thetank conveyor path 32 and thereturn path 33, which is both below thetank conveyor path 32, are positioned below theprocess fluid level 24 of theprocess tank 2. Consequently, theprocess tank conveyor 6 is submerged in a level of coating material equal to theprocess fluid level 24 inside the process tank when theprocess tank 2 is in operation. As a result, thearticle 50 traveling on the submergedprocess tank conveyor 6 will also be submerged in a level of coating material equal to theprocess fluid level 24, which results in the coating of thearticle 50. - According to the
system 1 of the present invention, theprocess tank conveyor 6 is configured to transfer anarticle 50 through theprocess tank 2. Referring toFigs. 1 and4 , aprocess tank conveyor 6 is shown. Theprocess tank conveyor 6 comprises a plurality ofhanger elements 19, a processtank conveyor track 28, andhardware 26 characterized by differential movement, i.e., parts that move relative to one another. Thehardware 26 connects thehanger elements 19 to the processtank conveyor track 28. Thehanger elements 19 are adapted to receive and support thearticle 50 while thearticle 50 is transferred through theprocess tank 2. According to one embodiment as shown infig. 1 , thehanger element 19 comprises twoslanted legs 20 connected to abase member 21 with a saw tooth edge 22 on the inner side of thebase member 21. When traveling through theprocess tank 2 on theprocess tank conveyor 6, thearticle 50 rests on thesaw tooth edge 22. In addition to electrically grounding the article, thesaw tooth edge 22 reduces the amount of surface area in contact with thearticle 50, as opposed to a flat edge. Thus, thesaw tooth edge 22 provides a greater surface area exposed to the coating material within theprocess tank 2. The hanger element utilizes slantedlegs 20, because theseslanted legs 20 provide improved clearance when traveling in thetank conveyor path 32. In a further embodiment, theprocess tank conveyor 6 may be configured such that thehanger 19 will remain positioned below theprocess fluid level 24, while thehardware 26 is located above theprocess fluid level 24 to prevent hardware malfunction due to coating material build-up or corrosion. - Moreover, the
process tank 2 comprises at least oneelectrode 10 configured to provide a charge to the coating material inside theprocess tank 2. As shown inFig. 2 , theprocess tank 2 may comprise a plurality ofelectrodes 10. Theelectrodes 10 are operable for anodic or cathodic coating. Theprocess tank conveyor 6 holds thearticle 50, which typically comprises a rail or other elongated article, at an electrical potential. Under anodic coating, a positively chargedarticle 50 is passed through theprocess tank 2 on theprocess tank conveyor 6. To bind the coating material to thearticle 50, theelectrode 10 must provide thecoating material 22 with a negative charge, so that the positively chargedarticle 50 may bind with the negatively charged coating. Conversely, under cathodic coating, theprocess tank 2 receives a negatively chargedarticle 50; therefore, theelectrode 10 must provide a positive charge to thecoating material 22 to ensure binding between thearticle 50 and thecoating material 22. -
Fig. 3 further illustrates thesystem 1 of the present invention, wherein aninput conveyor 42 and anoutput conveyor 44 are in communication with theprocess tank 2. Theinput conveyor 42 is located adjacent to theentry port 8, and theoutput conveyor 44 is located adjacent to theexit port 9. Theinput 42 andoutput 44 conveyors define input/output conveyor paths that are independent of the process tank conveyor path. In this manner, theinput conveyor 42 andoutput conveyor 44 operate independently of theprocess tank 2 and theprocess tank conveyor 6. Theinput conveyor 42 feeds anarticle 50 into theentry port 8 of theprocess tank 6 wherein thearticle 50 will then be received by theprocess tank conveyor 6 for coating. Subsequently, theoutput conveyor 44 receives thecoated article 50 as it is outputted from the process tank through theexit port 9 by theprocess tank conveyor 6. This three conveyor system comprised of theinput conveyor 42,process tank conveyor 6, and theoutput conveyor 44 enables thesystem 1 to run continuously without regard to the length of thearticle 50 being fed into thesystem 1, or the nature of theinput 42 andoutput 44 conveyors being used. - In a preferred embodiment, a
system 1 for electrocoating anarticle 50 of variable length is provided. Thesystem 1 includes aprocess tank 2 comprising anentry port 8, and exitport 9 opposite theentry port 8, and aprocess path 30 extending from theentry port 8 to theexit port 9. Theprocess tank 2 further comprises an open-endedprocess tank conveyor 6 at least partially positioned below aprocess fluid level 24 defined by theprocess tank 2. The open-endedprocess tank conveyor 6, which is disposed entirely within theprocess tank 2, defines atank conveyor path 32 extending from a receivingend 46 of theprocess tank conveyor 6 to a dispensingend 48 of theprocess tank conveyor 6 along at least a portion of theprocess path 30, wherein theprocess tank conveyor 2 comprises an open-ended configuration at the receivingend 46 of theprocess tank conveyor 6 and an open-ended configuration at the dispensingend 48 of theprocess tank conveyor 6. Furthermore, thesystem 1 also comprises acoating material supply 4 in communication with theprocess tank 2, aninput conveyor 42 adapted to feed thearticle 50 into theprocess tank 2, and anoutput conveyor 44 adapted to receive acoated article 50 from theprocess tank 2. - In another embodiment, the
coating system 1 may comprise additional processing stations for thearticle 50 being coated. The system may incorporate heat exchangers, which are useful in the electrocoating process wherein operating temperatures may vary. The system may also include cleaning stations and pretreatment stations to prepare the surface of anarticle 50 for coating. Pretreatment stations include phosphate baths. Rinsing stations may be incorporated into the system to remove paint solids from the coating, which may affect the efficiency and the aesthetic appeal of the coating. The system may also comprise curing ovens, which cures and cross links the coating material after the coating has been applied to assure maximum performance properties of the coating. The system may further comprise water conditioning stations, or any other suitable processing station known to one of ordinary skill in the art. All of the processing stations may be used singularly or in combination with the coating system of the present invention. - In a further embodiment of the present invention, a method for electrocoating is provided. The coating method is applicable to anodic or cathodic coating. The electrocoating method comprises the steps of providing and loading an
article 50, such as a rail, onto aninput conveyor 42, and subsequently inputting thearticle 50 into aprocess tank 2 through anentry port 8. Subsequently, thearticle 50 is transferred through theprocess tank 2 by aprocess tank conveyor 6, wherein thearticle 50 is simultaneously coated as it moves through theprocess tank 2. After coating, theprocess tank conveyor 6 outputs thecoated article 50 through anexit port 9 in theprocess tank 2 wherein thecoated article 50 is then received by anoutput conveyor 44. The method incorporates any additional processing steps like pretreating, cleaning, heating, preheating, rinsing, curing, and any combinations thereof. - It is noted that terms like "preferably," "commonly," and "typically" and the like are not utilized herein to limit the scope of the claimed invention or to imply that certain features are critical, essential, or even important to the structure or function of the claimed invention. Rather, these terms are merely intended to highlight alternative or additional features that may or may not be utilized in a particular embodiment of the present invention.
- For the purposes of describing and defining the present invention it is noted that the term "device" is utilized herein to represent a combination of components and individual components, regardless of whether the components are combined with other components.
- Having described the invention in detail and by reference to specific embodiments thereof, it will be apparent that modifications and variations are possible without departing from the scope of the invention defined in the appended claims. More specifically, although some aspects of the present invention are identified herein as preferred or particularly advantageous, it is contemplated that the present invention is not necessarily limited to these preferred aspects of the invention.
Claims (18)
- A system for coating comprising:a process tank, the process tank comprising an entry port, an exit port opposite the entry port, and a process path extending from the entry port to the exit port;an open-ended process tank conveyor disposed entirely within the process tank and comprising a track, a plurality of hanger elements coupled to the track and configured to support an article thereon, and hardware characterized by differential movement configured to connect the hanger elements to the track, wherein the track and hanger elements of the conveyor are configured to move characterized by a tank conveyor path vertically spaced above a return path, wherein the hanger elements are arranged below a process fluid level defined by the process tank; anda coating material supply in communication with the process tank, wherein the coating material supply comprises an overflow tank in fluid communication with the process tank.
- A system according to claim 1 wherein the hanger elements comprise at least two legs, and a base member connecting the legs, the base member adapted to hold an article.
- A system according to claim 2 wherein the base member comprises a saw tooth edge configured to support the article.
- A system according to claim 1 wherein the process tank entry port and the process tank exit port are positioned at least partially below the process fluid level defined by the process tank.
- A system according to claim 1 wherein the return path extends from the dispensing end of the process tank conveyor to the receiving end of the process tank conveyor.
- A system according to claim 5 wherein the tank conveyor path and return path are positioned at least partially below a process fluid level defined by the process tank.
- A system according to claim 1 wherein the process tank comprises at least one electrode configured to provide an electrical charge to a coating material inside the process tank, and the process tank conveyor is configured to hold an article at a predetermined electrical potential inside the process tank.
- A system according to claim 1 wherein the differential movement hardware is positioned at least partially above a process fluid level defined by the process tank.
- A system according to claim 1 further comprising an input conveyor and an output conveyor, wherein:the input conveyor is configured to transfer an article from the input conveyor through the entry port of the process tank to the process tank conveyor;the output conveyor is configured to receive an article transferred from the process tank conveyor through the exit port of the process tank to the output conveyor;the input conveyor defines an input conveyor path that is independent of the process tank conveyor; andthe output conveyor defines an output conveyor path that is independent of the process tank conveyor.
- A system according to claim 9 wherein the system further comprises at least one additional processing station in direct or indirect communication with the input or output conveyor, the processing station selected from heat exchangers, cleaning stations, pretreatment stations, rinsing stations, curing ovens, water conditioning stations, and combinations thereof.
- A system according to claim 1 wherein:the overflow tank comprises at least one material supply pump configured to transfer fluid from the overflow tank to the process tank;the material supply pump defines a volumetric material supply rate; andthe entry port and the exit port are configured to permit fluid contained within the process tank to flow out of the process tank into the overflow tank at a volumetric flow rate that is lower than the volumetric material supply rate.
- A system according to claim 11 wherein:the process tank further comprises at least one overflow portion configured to permit fluid contained within the process tank to flow out of the process tank into the overflow tank; andthe volumetric flow rates are collectively defined by the overflow portion and the entry and exit ports, these volumetric flow rates are at least as large as the volumetric material supply rate defined by the material supply pump.
- A system according to claim 11 wherein the process tank comprises a separating wall between the process tank and the overflow tank.
- A system according to claim 13 wherein the process tank comprises stop gates adapted to close the entry port and the exit port and prevent coating material from flowing out of the process tank into the overflow tank.
- A system according to claim 11 wherein the coating material supply comprises an electrocoating fluid.
- A system according to claim 11 wherein the coating material comprises a liquid paint, a fluidized powder, or any combinations thereof.
- A method of electrocoating comprising:providing an article with a length that is greater than the maximum length dimension of the process tank;loading the article onto an input conveyor;inputting the article into a process tank through an entry port in the process tank;transferring the article through the process tank by an open-ended process tank conveyor, wherein the open-ended process tank conveyor comprises a track, a plurality of hanger elements coupled to the track and supporting the article thereon, and hardware characterized by differential movement connecting the hanger elements to the track;coating the article with a coating material supply in communication with the process tank as the article is transferred through the process tank characterized by a tank conveyor path vertically spaced above a return path, wherein the hanger elements and the article supported thereon are submerged below the level of coating material in the process tank, wherein the coating material supply comprises an overflow tank in fluid communication with the process tank;outputting the coated article out of the process tank through an exit port in the process tank; andreceiving the coated article by an output conveyor adjacent to the exit port of the process tank.
- A method according to claim 17 wherein the process tank entry port and the exit port of the process tank are configured to permit fluid contained within the process tank to flow out of the process tank into the overflow tank at a volumetric flow rate that is lower than a volumetric material supply rate provided by the coating material supply.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL05812128T PL1920085T3 (en) | 2004-11-30 | 2005-10-13 | Continuous coating process |
Applications Claiming Priority (3)
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US63180504P | 2004-11-30 | 2004-11-30 | |
US11/158,221 US7241366B2 (en) | 2004-11-30 | 2005-06-21 | Continuous coating process |
PCT/US2005/037085 WO2006060067A2 (en) | 2004-11-30 | 2005-10-13 | Continuous coating process |
Publications (3)
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EP1920085A2 EP1920085A2 (en) | 2008-05-14 |
EP1920085A4 EP1920085A4 (en) | 2010-10-06 |
EP1920085B1 true EP1920085B1 (en) | 2012-05-23 |
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EP05812128A Active EP1920085B1 (en) | 2004-11-30 | 2005-10-13 | Continuous coating process |
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US (1) | US7241366B2 (en) |
EP (1) | EP1920085B1 (en) |
BR (1) | BRPI0503727B1 (en) |
PL (1) | PL1920085T3 (en) |
WO (1) | WO2006060067A2 (en) |
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DE102008047704B4 (en) * | 2008-09-18 | 2017-03-30 | GM Global Technology Operations LLC (n. d. Ges. d. Staates Delaware) | Device for dip painting a body part |
US20120097101A1 (en) * | 2010-04-23 | 2012-04-26 | Metokote Corporation | Modularly Integrated Coating Systems |
KR102006845B1 (en) * | 2019-04-18 | 2019-08-05 | 주식회사 스틸티앤씨 | Electrode Coating System for prevent oxidation |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2829762A (en) * | 1956-01-16 | 1958-04-08 | Alvey Conveyor Mfg Company | Live conveyor |
US3658677A (en) | 1969-12-22 | 1972-04-25 | American Can Co | Electroflow method of electrocoating |
US4401522A (en) * | 1980-09-29 | 1983-08-30 | Micro-Plate, Inc. | Plating method and apparatus |
DE3230660C1 (en) | 1982-08-02 | 1984-01-26 | Basf Farben + Fasern Ag, 2000 Hamburg | Method and device for carrying out electro-dipping and application |
JPS5985897A (en) | 1982-11-06 | 1984-05-17 | Nippon Paint Co Ltd | Method and device for adjusting electrodeposition paint bath |
US4663014A (en) | 1986-01-02 | 1987-05-05 | I. Jay Bassett | Electrodeposition coating apparatus |
US6139708A (en) | 1987-08-08 | 2000-10-31 | Nissan Motor Co., Ltd. | Dip surface-treatment system and method of dip surface-treatment using same |
EP0361029B1 (en) * | 1988-09-01 | 1993-05-19 | Siemens Nixdorf Informationssysteme Aktiengesellschaft | Electroplating apparatus for planar work pieces, particularly circuit boards |
DE3836256A1 (en) * | 1988-10-25 | 1990-04-26 | Schering Ag | DEVICE FOR GALVANIZING OR CHEMICAL TREATING METAL PARTS |
US6342146B1 (en) | 1995-07-14 | 2002-01-29 | Geronimo Z. Velasquez | Lead-free alloy plating method |
DE19713203C1 (en) * | 1997-03-28 | 1998-11-12 | Nuetro Maschinen & Anlagen | Device and method for surface treatment by dipping |
US6223890B1 (en) | 1997-11-11 | 2001-05-01 | Metokote Corporation | Conveyor system |
DE19834245B4 (en) * | 1998-07-29 | 2007-05-03 | Nütro Maschinen- und Anlagenbau GmbH & Co. KG | Device for electrolytic coating |
US6153064A (en) * | 1998-11-25 | 2000-11-28 | Oliver Sales Company | Apparatus for in line plating |
US20030052009A1 (en) * | 2001-09-14 | 2003-03-20 | Case Leo L. | Method and apparatus for the bulk coating of components |
DE10153171B4 (en) * | 2001-10-27 | 2004-09-16 | Atotech Deutschland Gmbh | Method and device for the electrolytic treatment of parts in continuous systems |
-
2005
- 2005-06-21 US US11/158,221 patent/US7241366B2/en active Active
- 2005-09-19 BR BRPI0503727-1A patent/BRPI0503727B1/en active IP Right Grant
- 2005-10-13 WO PCT/US2005/037085 patent/WO2006060067A2/en active Application Filing
- 2005-10-13 PL PL05812128T patent/PL1920085T3/en unknown
- 2005-10-13 EP EP05812128A patent/EP1920085B1/en active Active
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EP1920085A4 (en) | 2010-10-06 |
PL1920085T3 (en) | 2012-11-30 |
US7241366B2 (en) | 2007-07-10 |
WO2006060067A3 (en) | 2006-11-23 |
US20060113183A1 (en) | 2006-06-01 |
WO2006060067B1 (en) | 2007-01-25 |
WO2006060067A2 (en) | 2006-06-08 |
BRPI0503727A (en) | 2006-07-11 |
BRPI0503727B1 (en) | 2015-06-30 |
EP1920085A2 (en) | 2008-05-14 |
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